CN206184438U - Liquid -phase hydrogenated reactor - Google Patents

Liquid -phase hydrogenated reactor Download PDF

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Publication number
CN206184438U
CN206184438U CN201621233379.1U CN201621233379U CN206184438U CN 206184438 U CN206184438 U CN 206184438U CN 201621233379 U CN201621233379 U CN 201621233379U CN 206184438 U CN206184438 U CN 206184438U
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liquid
heat exchange
motor
exchange tube
hydrogenation reactor
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Expired - Fee Related
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CN201621233379.1U
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Chinese (zh)
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王平均
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Jingjiang City Environmental Protection Technology Co Ltd
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Jingjiang City Environmental Protection Technology Co Ltd
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Abstract

The utility model discloses a liquid -phase hydrogenated reactor, including the barrel, be equipped with the motor directly over the barrel, the (mixing) shaft is connected to the motor, is equipped with stirring vane on the (mixing) shaft, and the motor both sides are equipped with manhole and hydrogenation hole, set up the baffle in the barrel, and the baffle below is equipped with the heat exchange tube that spirals and appear, and stirring vane's height is the same with heat exchange tube lower extreme height, and both ends are equipped with steam inlet respectively and are equipped with feed inlet, discharge gate, catalyst inlet with condensation export, barrel side about the heat exchange tube, are equipped with the emptying mouth below the barrel, the emptying mouth outside is equipped with the shrouding, liquid -phase hydrogenated reactor, structure science, the heat exchange tube setting is used with the agitator cooperation at the middle part, the heat exchange distribution of temperature is even, has improved feed stock conversion and product quality.

Description

一种液相加氢反应器A liquid phase hydrogenation reactor

技术领域technical field

本实用新型属于化工设备技术领域,具体涉及一种液相加氢反应器。The utility model belongs to the technical field of chemical equipment, in particular to a liquid-phase hydrogenation reactor.

背景技术Background technique

加氢反应器是化工行业重要的设备之一,目前加氢反应器使用过程中存在两个缺陷:1、结构复杂,存在运行可靠性不理想、使用寿命短、反应效率低等缺陷,2、原来使用导热油作为热交换介质,导热油由加氢反应器顶部进入,与上升的物料形成对流进行换热,由中部流出将大量的反应热带走;此工艺由于导热油不能将反应器完全充满,导致上下部分温度分布不均,不能起到最佳的催化作用,若温度低于反应温度,催化剂失去催化作用,造成原料利用率下降,降低产品质量,需要进一步加以改进。The hydrogenation reactor is one of the important equipment in the chemical industry. At present, there are two defects in the use of the hydrogenation reactor: 1. The structure is complex, and there are defects such as unsatisfactory operation reliability, short service life, and low reaction efficiency. 2. Originally, heat transfer oil was used as the heat exchange medium. The heat transfer oil enters from the top of the hydrogenation reactor, forms a convection flow with the rising material for heat exchange, and flows out from the middle to take away a large amount of reaction heat. In this process, the heat transfer oil cannot completely fill the reactor. , leading to uneven temperature distribution in the upper and lower parts, which cannot play the best catalytic effect. If the temperature is lower than the reaction temperature, the catalyst will lose its catalytic effect, resulting in a decrease in the utilization rate of raw materials and a reduction in product quality, which needs further improvement.

发明内容Contents of the invention

为解决上述问题,本实用新型公开了一种液相加氢反应器,结构科学,热交换时温度分布均匀,提高了原料转化率和产品质量。In order to solve the above problems, the utility model discloses a liquid-phase hydrogenation reactor, which has a scientific structure, uniform temperature distribution during heat exchange, and improved raw material conversion rate and product quality.

为达到上述目的,本实用新型的技术方案如下:In order to achieve the above object, the technical scheme of the utility model is as follows:

一种液相加氢反应器,其特征在于:包括筒体,筒体正上方设有电机,所述电机连接搅拌轴,搅拌轴上设有搅拌叶片,电机两侧设有人孔与加氢孔,筒体内设置隔板,隔板下方设有盘旋形的换热管,搅拌叶片的高度与换热管下端高度相同,换热管上下两端分别设有蒸汽进口与冷凝出口,筒体侧面设有进料口、出料口、催化剂进口,筒体下方设有排净口,所述排净口外侧设有封板。A liquid-phase hydrogenation reactor, characterized in that it includes a cylinder, a motor is provided directly above the cylinder, the motor is connected to a stirring shaft, a stirring blade is provided on the stirring shaft, manholes and hydrogenation holes are provided on both sides of the motor , there is a partition in the cylinder, and a spiral heat exchange tube is arranged under the partition. The height of the stirring blade is the same as the height of the lower end of the heat exchange tube. There are material inlet, material outlet and catalyst inlet, and the bottom of the cylinder is provided with a discharge port, and the outside of the discharge port is provided with a sealing plate.

作为本实用新型的一种改进,所述电机一侧设有排气口。As an improvement of the utility model, an exhaust port is provided on one side of the motor.

作为本实用新型的一种改进,所述加氢孔上设有流量表。As an improvement of the utility model, a flow meter is provided on the hydrogenation hole.

作为本实用新型的一种改进,所述筒体内壁设有防腐层。As an improvement of the utility model, an anti-corrosion layer is provided on the inner wall of the cylinder.

作为本实用新型的一种改进,所述排净口一侧设有带热电偶温度计。As an improvement of the utility model, a thermometer with a thermocouple is provided on one side of the drain port.

作为本实用新型的一种改进,所述排净口一侧设有取样口。As an improvement of the utility model, a sampling port is provided on one side of the cleaning port.

作为本实用新型的一种改进,所述筒体外侧设有吊耳。As an improvement of the utility model, lifting lugs are provided on the outer side of the cylinder.

本实用新型的有益效果是:The beneficial effects of the utility model are:

本实用新型所述的一种液相加氢反应器,结构科学,换热管设置在中部,与搅拌器配合使用,热交换温度分布均匀,提高了原料转化率和产品质量。The liquid-phase hydrogenation reactor described in the utility model has a scientific structure, and the heat exchange tube is arranged in the middle, used together with the stirrer, the heat exchange temperature is evenly distributed, and the conversion rate of raw materials and product quality are improved.

附图说明Description of drawings

图1为本实用新型的结构示意图。Fig. 1 is the structural representation of the utility model.

附图标记列表:List of reference signs:

1、筒体,2、电机,3、搅拌轴,4、搅拌叶片,5、人孔,6、加氢孔,7、隔板,8、换热管,9、蒸汽进口,10、冷凝出口,11、进料口,12、出料口,13、催化剂进口,14、排净口,15、封板,16、排气口,17、流量表,18、带热电偶温度计,19、取样口,20、吊耳。1. Cylinder, 2. Motor, 3. Stirring shaft, 4. Stirring blade, 5. Manhole, 6. Hydrogenation hole, 7. Separator, 8. Heat exchange tube, 9. Steam inlet, 10. Condensation outlet , 11, material inlet, 12, material outlet, 13, catalyst inlet, 14, net discharge port, 15, sealing plate, 16, exhaust port, 17, flow meter, 18, thermometer with thermocouple, 19, sampling Mouth, 20, lugs.

具体实施方式detailed description

下面结合附图和具体实施方式,进一步阐明本实用新型,应理解下述具体实施方式仅用于说明本实用新型而不用于限制本实用新型的范围。需要说明的是,下面描述中使用的词语“前”、“后”、“左”、“右”、“上”和“下”指的是附图中的方向,词语“内”和“外”分别指的是朝向或远离特定部件几何中心的方向。The utility model will be further explained below in conjunction with the accompanying drawings and specific embodiments. It should be understood that the following specific embodiments are only used to illustrate the utility model and are not intended to limit the scope of the utility model. It should be noted that the words "front", "rear", "left", "right", "upper" and "lower" used in the following description refer to the directions in the drawings, and the words "inner" and "outer ” refer to directions toward or away from the geometric center of a particular part, respectively.

如图所示,本实用新型所述的一种液相加氢反应器,包括筒体1,筒体1正上方设有电机2,所述电机2连接搅拌轴3,搅拌轴3上设有搅拌叶片4,电机2两侧设有人孔5与加氢孔6,筒体1内设置隔板7,隔板7下方设有盘旋形的换热管8,搅拌叶片4的高度与换热管8下端高度相同,换热管8上下两端分别设有蒸汽进口9与冷凝出口10,筒体1侧面设有进料口11、出料口12、催化剂进口13,筒体下方设有排净口14,所述排净口14外侧设有封板15。As shown in the figure, a liquid-phase hydrogenation reactor described in the utility model includes a cylinder body 1, a motor 2 is provided directly above the cylinder body 1, and the motor 2 is connected to a stirring shaft 3, and a stirring shaft 3 is provided with Stirring blades 4, manholes 5 and hydrogenation holes 6 are provided on both sides of the motor 2, a partition 7 is provided in the cylinder body 1, and a spiral heat exchange tube 8 is provided below the partition 7. The height of the stirring blade 4 and the heat exchange tube 8. The height of the lower end is the same. The upper and lower ends of the heat exchange tube 8 are provided with a steam inlet 9 and a condensation outlet 10 respectively. Port 14, and a sealing plate 15 is provided on the outside of the drain port 14.

本实用新型所述的一种液相加氢反应器,结构科学,使用方便,换热管设置在中部,与搅拌器配合使用,热交换温度分布均匀,提高了原料转化率和产品质量。The liquid-phase hydrogenation reactor described in the utility model has a scientific structure and is easy to use. The heat exchange tube is arranged in the middle and used in conjunction with the stirrer. The heat exchange temperature is evenly distributed, and the conversion rate of raw materials and product quality are improved.

本实用新型所述电机2一侧设有排气口16。One side of the motor 2 described in the utility model is provided with an exhaust port 16 .

本实用新型所述加氢孔6上设有流量表17。The hydrogenation hole 6 of the utility model is provided with a flow meter 17 .

本实用新型所述筒体1内壁设有防腐层,耐腐蚀,延长使用寿命。The inner wall of cylinder body 1 described in the utility model is provided with an anti-corrosion layer, which is corrosion-resistant and prolongs the service life.

本实用新型所述排净口14一侧设有带热电偶温度计18。One side of the discharge port 14 described in the utility model is provided with a thermometer 18 with a thermocouple.

本实用新型所述排净口14一侧设有取样口19。A sampling port 19 is provided on one side of the discharge port 14 described in the utility model.

本实用新型所述筒体1外侧设有吊耳20。The outer side of the cylindrical body 1 of the utility model is provided with lifting lugs 20 .

本实用新型方案所公开的技术手段不仅限于上述实施方式所公开的技术手段,还包括由以上技术特征任意组合所组成的技术方案。The technical means disclosed in the solution of the utility model are not limited to the technical means disclosed in the above embodiments, but also include technical solutions composed of any combination of the above technical features.

Claims (7)

1.一种液相加氢反应器,其特征在于:包括筒体,筒体正上方设有电机,所述电机连接搅拌轴,搅拌轴上设有搅拌叶片,电机两侧设有人孔与加氢孔,筒体内设置隔板,隔板下方设有盘旋形的换热管,搅拌叶片的高度与换热管下端高度相同,换热管上下两端分别设有蒸汽进口与冷凝出口,筒体侧面设有进料口、出料口、催化剂进口,筒体下方设有排净口,所述排净口外侧设有封板。1. A liquid-phase hydrogenation reactor, characterized in that: it comprises a cylinder, a motor is arranged directly above the cylinder, the motor is connected to a stirring shaft, a stirring blade is provided on the stirring shaft, and manholes and fuel tanks are arranged on both sides of the motor. Hydrogen holes, a partition is set in the cylinder, and a spiral heat exchange tube is arranged under the partition. The height of the stirring blade is the same as the height of the lower end of the heat exchange tube. The side is provided with a material inlet, a material outlet, and a catalyst inlet, and a discharge port is provided at the bottom of the cylinder, and a sealing plate is provided outside the discharge port. 2.根据权利要求1所述的一种液相加氢反应器,其特征在于:所述电机一侧设有排气口。2. A liquid-phase hydrogenation reactor according to claim 1, wherein an exhaust port is provided on one side of the motor. 3.根据权利要求1所述的一种液相加氢反应器,其特征在于:所述加氢孔上设有流量表。3. A liquid-phase hydrogenation reactor according to claim 1, characterized in that: said hydrogenation hole is provided with a flow meter. 4.根据权利要求1所述的一种液相加氢反应器,其特征在于:所述筒体内壁设有防腐层。4. A liquid-phase hydrogenation reactor according to claim 1, characterized in that: the inner wall of the cylinder is provided with an anti-corrosion layer. 5.根据权利要求1所述的一种液相加氢反应器,其特征在于:所述排净口一侧设有带热电偶温度计。5. A liquid-phase hydrogenation reactor according to claim 1, characterized in that: a thermometer with a thermocouple is provided on one side of the drain port. 6.根据权利要求1所述的一种液相加氢反应器,其特征在于:所述排净口一侧设有取样口。6 . The liquid-phase hydrogenation reactor according to claim 1 , wherein a sampling port is provided on one side of the drain port. 7 . 7.根据权利要求1所述的一种液相加氢反应器,其特征在于:所述筒体外侧设有吊耳。7. A liquid-phase hydrogenation reactor according to claim 1, characterized in that: lifting lugs are provided on the outside of the cylinder.
CN201621233379.1U 2016-11-17 2016-11-17 Liquid -phase hydrogenated reactor Expired - Fee Related CN206184438U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201621233379.1U CN206184438U (en) 2016-11-17 2016-11-17 Liquid -phase hydrogenated reactor

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Application Number Priority Date Filing Date Title
CN201621233379.1U CN206184438U (en) 2016-11-17 2016-11-17 Liquid -phase hydrogenated reactor

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Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108998081A (en) * 2018-09-18 2018-12-14 汤美侠 A method for optimizing the efficiency of diesel oil refining
CN108998079A (en) * 2018-09-03 2018-12-14 汤美侠 A kind of extraction process of light oil
CN109126667A (en) * 2018-09-03 2019-01-04 汤美侠 A kind of hydrogenator
CN110935413A (en) * 2019-12-11 2020-03-31 西安交通大学 A kind of acid leaching tank device for red mud acid leaching process and red mud acid leaching process method
CN114471411A (en) * 2022-02-11 2022-05-13 成都灿菱科技有限公司 Reation kettle is used in chemical product processing of high temperature accuse precision

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108998079A (en) * 2018-09-03 2018-12-14 汤美侠 A kind of extraction process of light oil
CN109126667A (en) * 2018-09-03 2019-01-04 汤美侠 A kind of hydrogenator
CN108998081A (en) * 2018-09-18 2018-12-14 汤美侠 A method for optimizing the efficiency of diesel oil refining
CN108998081B (en) * 2018-09-18 2020-12-04 临沂文衡信息技术有限公司 A method for optimizing diesel refining efficiency
CN110935413A (en) * 2019-12-11 2020-03-31 西安交通大学 A kind of acid leaching tank device for red mud acid leaching process and red mud acid leaching process method
CN114471411A (en) * 2022-02-11 2022-05-13 成都灿菱科技有限公司 Reation kettle is used in chemical product processing of high temperature accuse precision
CN114471411B (en) * 2022-02-11 2023-12-22 九江前发精细化工有限公司 Reaction kettle for processing chemical products with high temperature control precision

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Granted publication date: 20170524

Termination date: 20191117